A \(20 \mathrm{~mm} \times 20 \mathrm{~mm}\) silicon chip is mounted such that the edges are flush in a substrate. The substrate provides an unheated starting length of \(20 \mathrm{~mm}\) that acts as turbulator. Airflow at \(25^{\circ} \mathrm{C}(1 \mathrm{~atm})\) with a velocity of \(25 \mathrm{~m} / \mathrm{s}\) is used to cool the upper surface of the chip. If the maximum surface temperature of the chip cannot exceed \(75^{\circ} \mathrm{C}\), determine the maximum allowable power dissipation on the chip surface.

Short Answer

Expert verified
The maximum allowable power dissipation on the chip's surface is 5.67 W.

Step by step solution

01

Calculate important properties of the air

We're given the temperature (\(T_\infty = 25^{\circ} \mathrm{C}\)) and pressure (\(P_\infty = 1 \mathrm{~atm}\)) of the air in the system. At this pressure and temperature, we can look up the air's density (\(\rho\)), dynamic viscosity (\(\mu\)), thermal conductivity (\(k\)), and specific heat capacity (\(c_p\)) in a standard reference. The following properties can be found: \(\rho = 1.184 \mathrm{~kg/m^{3}}\) \(\mu = 1.846 \times 10^{-5} \mathrm{~Pa.s}\) \(k = 2.602 \times 10^{-2} \mathrm{~W/m.K}\) \(c_p = 1006 \mathrm{~J/kg.K}\)
02

Calculate the Reynolds number

The Reynolds number is calculated using the following formula: \(Re = \frac{\rho V L}{\mu}\) Where \(V = 25 \mathrm{~m/s}\) is the velocity of the air, \(L = 20 \mathrm{~mm}\) is the length of the chip, and \(\rho\) and \(\mu\) are the air properties we found in step 1. \(Re = \frac{(1.184 \mathrm{~kg/m^{3}}) \times (25 \mathrm{~m/s}) \times (20 \times 10^{-3} \mathrm{~m})}{(1.846 \times 10^{-5} \mathrm{~Pa.s})} = 32046\)
03

Calculate heat transfer coefficient (h) using Nusselt Number

For laminar flow over a flat plate, with a Reynolds number between 5000 and \(10^5\), we can use the following Nusselt number relation: \(Nu = 0.664Re^{0.5}Pr^{1/3}\) Where \(Nu\) is the Nusselt number, \(Re\) is the Reynolds number calculated in step 2, and \(Pr\) is the Prandtl number. The Prandtl number can be calculated using the following formula: \(Pr = \frac{c_p \mu}{k}\) \(Pr = \frac{(1006 \mathrm{~J/kg.K}) \times (1.846 \times 10^{-5} \mathrm{~Pa.s})}{(2.602 \times 10^{-2} \mathrm{~W/m.K})} = 0.707\) Inserting the values of \(Re\) and \(Pr\) into the Nusselt number relation: \(Nu = 0.664(32046)^{0.5}(0.707)^{1/3} = 217.8\) Now we can calculate the heat transfer coefficient (h) using the following formula: \(h = \frac{Nu \times k}{L}\) \(h = \frac{(217.8) \times (2.602 \times 10^{-2} \mathrm{~W/m.K})}{(20 \times 10^{-3} \mathrm{~m})} = 283.6 \mathrm{~W/m^2.K}\)
04

Calculate the maximum allowable heat flux

We can calculate the maximum allowable heat flux using the following relation: \(q'' = h(T_{max} - T_\infty)\) Where \(q''\) is the heat flux, \(h\) is the heat transfer coefficient we calculated in step 3, \(T_{max}\) is the maximum surface temperature (\(75^{\circ} \mathrm{C}\)), and \(T_\infty\) is the temperature of the air (\(25^{\circ} \mathrm{C}\)). \(q'' = (283.6 \mathrm{~W/m^2.K})(75-25) = 14180 \mathrm{~W/m^2}\)
05

Calculate the maximum allowable power dissipation

The maximum allowable power dissipation can be calculated using the following formula: \(P_{max} = q'' \times A\) Where \(P_{max}\) is the maximum allowable power dissipation, \(q''\) is the heat flux calculated in step 4, and \(A\) is the surface area of the chip. Since the chip is \(20 \mathrm{~mm} \times 20 \mathrm{~mm}\), the surface area is: \(A = (20 \times 10^{-3} \mathrm{~m}) \times (20 \times 10^{-3} \mathrm{~m}) = 4 \times 10^{-4} \mathrm{~m^2}\) Now, we can calculate the maximum allowable power dissipation: \(P_{max} = (14180 \mathrm{~W/m^2}) \times (4 \times 10^{-4} \mathrm{~m^2}) = 5.67 \mathrm{~W}\) Therefore, the maximum allowable power dissipation on the chip surface is 5.67 W.

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Most popular questions from this chapter

A heated long cylindrical rod is placed in a cross flow of air at \(20^{\circ} \mathrm{C}(1 \mathrm{~atm})\) with velocity of \(10 \mathrm{~m} / \mathrm{s}\). The rod has a diameter of \(5 \mathrm{~mm}\) and its surface has an emissivity of \(0.95\). If the surrounding temperature is \(20^{\circ} \mathrm{C}\) and the heat flux dissipated from the rod is \(16000 \mathrm{~W} / \mathrm{m}^{2}\), determine the surface temperature of the rod. Evaluate the air properties at \(70^{\circ} \mathrm{C}\).

Hot engine oil at \(150^{\circ} \mathrm{C}\) is flowing in parallel over a flat plate at a velocity of \(2 \mathrm{~m} / \mathrm{s}\). Surface temperature of the \(0.5-\mathrm{m}-\) long flat plate is constant at \(50^{\circ} \mathrm{C}\). Determine \((a)\) the local convection heat transfer coefficient at \(0.2 \mathrm{~m}\) from the leading edge and the average convection heat transfer coefficient, and (b) repeat part ( \(a\) ) using the Churchill and Ozoe (1973) relation.

Consider a house that is maintained at a constant temperature of \(22^{\circ} \mathrm{C}\). One of the walls of the house has three singlepane glass windows that are \(1.5 \mathrm{~m}\) high and \(1.8 \mathrm{~m}\) long. The glass \((k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is \(0.5 \mathrm{~cm}\) thick, and the heat transfer coefficient on the inner surface of the glass is \(8 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Now winds at \(35 \mathrm{~km} / \mathrm{h}\) start to blow parallel to the surface of this wall. If the air temperature outside is \(-2^{\circ} \mathrm{C}\), determine the rate of heat loss through the windows of this wall. Assume radiation heat transfer to be negligible. Evaluate the air properties at a film temperature of \(5^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\).

A long 8-cm-diameter steam pipe whose external surface temperature is \(90^{\circ} \mathrm{C}\) passes through some open area that is not protected against the winds. Determine the rate of heat loss from the pipe per unit of its length when the air is at \(1 \mathrm{~atm}\) pressure and \(7^{\circ} \mathrm{C}\) and the wind is blowing across the pipe at a velocity of \(50 \mathrm{~km} / \mathrm{h}\).

Liquid mercury at \(250^{\circ} \mathrm{C}\) is flowing in parallel over a flat plate at a velocity of \(0.3 \mathrm{~m} / \mathrm{s}\). Surface temperature of the \(0.1-\mathrm{m}\)-long flat plate is constant at \(50^{\circ} \mathrm{C}\). Determine \((a)\) the local convection heat transfer coefficient at \(5 \mathrm{~cm}\) from the leading edge and \((b)\) the average convection heat transfer coefficient over the entire plate.

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